US6602414B2 - Molecule separation device and method combining multiple filtration media - Google Patents

Molecule separation device and method combining multiple filtration media Download PDF

Info

Publication number
US6602414B2
US6602414B2 US09/818,468 US81846801A US6602414B2 US 6602414 B2 US6602414 B2 US 6602414B2 US 81846801 A US81846801 A US 81846801A US 6602414 B2 US6602414 B2 US 6602414B2
Authority
US
United States
Prior art keywords
molecule
separator device
collection
molecules
membrane
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related, expires
Application number
US09/818,468
Other versions
US20010025818A1 (en
Inventor
Timothy Neal Warner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FORMULATION PRO
Formulations Pro
Original Assignee
Formulations Pro
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Formulations Pro filed Critical Formulations Pro
Priority to US09/818,468 priority Critical patent/US6602414B2/en
Assigned to FORMULATION PRO reassignment FORMULATION PRO ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: WARNER, TIMOTHY NEAL
Publication of US20010025818A1 publication Critical patent/US20010025818A1/en
Priority to US10/460,280 priority patent/US7045064B2/en
Application granted granted Critical
Publication of US6602414B2 publication Critical patent/US6602414B2/en
Adjusted expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28033Membrane, sheet, cloth, pad, lamellar or mat
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/145Ultrafiltration
    • B01D61/146Ultrafiltration comprising multiple ultrafiltration steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/18Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/16Rotary, reciprocated or vibrated modules
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28023Fibres or filaments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28052Several layers of identical or different sorbents stacked in a housing, e.g. in a column
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01LCHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L3/00Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
    • B01L3/50Containers for the purpose of retaining a material to be analysed, e.g. test tubes
    • B01L3/502Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
    • B01L3/5021Test tubes specially adapted for centrifugation purposes
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/34Purifying; Cleaning
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/405Concentrating samples by adsorption or absorption
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4005Concentrating samples by transferring a selected component through a membrane
    • G01N2001/4016Concentrating samples by transferring a selected component through a membrane being a selective membrane, e.g. dialysis or osmosis
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T436/00Chemistry: analytical and immunological testing
    • Y10T436/25Chemistry: analytical and immunological testing including sample preparation
    • Y10T436/25375Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.]
    • Y10T436/255Liberation or purification of sample or separation of material from a sample [e.g., filtering, centrifuging, etc.] including use of a solid sorbent, semipermeable membrane, or liquid extraction

Definitions

  • This invention relates in general to the separation and capture of molecule types from a solution mixture thereof, and in particular to apparatus and methodology wherein molecules with two or more defined properties such as ionic, hydrophobic, or affinity attractions and molecular weight ranges are captured and retained first for one such property and thereafter for the additional property, with such respective collections accomplished sequentially in a single molecule separator device.
  • filter media are filter membranes and matrices thereof whose interstices prohibit, and thus capture, particulate whose physical size is too large to pass through as part of the solute.
  • Another object of the present invention to provide a molecule separator device where such molecule separation is accomplished sequentially within a single housing.
  • Yet another object of the present invention to provide a molecule separator device where respective dedicated membrane media provide filtrate collection.
  • Still another object of the present invention is to provide methodology for separating and capturing molecules having a plurality of properties utilizing a single separator device.
  • the present invention is a molecule separator device for separating and isolating molecules having at least two separable properties and present in a solution comprising the molecules.
  • the separator device includes a housing for accepting pressured passage there through of the solution, and at least two molecule collection media disposed within the housing, wherein each such medium captures molecules exhibiting a respective property respectively capturable by the media.
  • a first molecule-collection chromatography membrane captures and retains only molecules with an ionic, hydrophobic, or affinity attraction property while a second molecule-collection ultrafiltration membrane captures and retains additional such molecules that additionally fall within a particular molecular weight range.
  • a preferred housing is generally cylindrical for operational acceptance within a generally cylindrical fixed-angle or swinging-bucket chamber of a centrifuge head, and is constructed of a plurality of liquid-tight, releasably-connected compartments in communication with each other.
  • the collection media is situated in a sequential relationship among the compartments while centrifugation of the housing drives the solution through the media.
  • Removing and replacing appropriate compartments during the molecule collection process permits separate and replaceable reservoir, wash, and collection sites to yield filtrate product as so chosen for further analysis, processing, or use, or for discard where a separation goal is the provision of clean solute. Because of separation and subsequent collection of molecules bearing two or more properties, the present invention permits rapid and efficient isolation of molecules and/or micro-particulate having multiple identification characteristics.
  • FIG. 1 is a perspective view of a first embodiment of a molecule separator device for capture or collection of molecules and/or micro-particulate;
  • FIG. 2 is a perspective view of a separated compartment structure for the separator device of FIG. 1;
  • FIGS. 3 a - 3 e illustrate use of the embodiment of FIG. 1;
  • FIG. 4 is a side perspective view of a second embodiment of a molecule separator device.
  • FIGS. 5 a - 5 g illustrate use of the embodiment of FIG. 4 .
  • the device 10 includes a housing 12 constructed of two releasably connected, liquid-tight, separable compartments 14 , 16 attached to each other by conventional friction fit between adjacent compartments.
  • a housing 12 constructed of two releasably connected, liquid-tight, separable compartments 14 , 16 attached to each other by conventional friction fit between adjacent compartments.
  • the first membrane 24 is a chromatography membrane operating as a cationic or anionic ion-exchange membrane, hydrophobic membrane, affinity membrane, or a combination thereof for attracting molecules exhibiting ionic and/or hydrophobic and/or affinity attractions.
  • the first membrane 24 can have a porosity non-limitedly exemplified in the range of 0.1 to 10 microns and is fabricated of any appropriate microporous material including nylon, polycarbonate, polyethersulfone, glass fiber, polypropylene, polysulfone, cellulose acetate, regenerated cellulose, and mixed esters of cellulose or other polymeric material as would be recognized by a skilled artisan.
  • the second membrane 26 preferably is anisotropic (asymmetrical) and can be fabricated of the same materials as the first while providing ultrafiltration in speaking toward molecular weight characteristics for capturing molecule filtrate.
  • a chosen molecular weight range can be exemplified in values from about 5 ⁇ 10 2 to about 3 ⁇ 10 6 Daltons.
  • the upper compartment 14 of the housing 12 has an upper reservoir chamber 28 immediately above the first membrane 24 and a lower reservoir chamber 30 immediately below the first membrane 24 .
  • the lower compartment 16 includes an upper chamber 32 immediately above the second membrane 26 and a fluid collection chamber 34 immediately beneath the second membrane 26 .
  • FIG. 2 shows an independent compartment 36 attachable to the upper compartment 14 during certain washing procedures as described later.
  • the housing 12 can be constructed of a semi-rigid material such as polypropylene or of any other plastic or polymeric material as would be evident to a skilled artisan. Likewise, housing size can be as required to provide volumetric accommodations as required for a particular task.
  • a screw-type closure cap 38 with an aperture 40 there through closes the housing 12 .
  • the housing 12 resembles the configuration of a standard centrifuge tube, thus permitting placement of the separator device 10 within a standard fixed-angle or swinging-bucket chamber (not shown) of a centrifuge head (not shown). While centrifugation is the preferred manner of pressurized force, the aperture 40 in the screw cap 38 is provided to accept a pressure nozzle such as the outlet of a hypodermic syringe (not shown) whose pressure can be applied to force the solution through the separator device 10 .
  • FIGS. 3 a - 3 e A description of an exemplary operation of the separator device 10 is accompanied by the illustrations of FIGS. 3 a - 3 e .
  • the upper compartment 14 and an independent compartment 36 are attached as shown in FIGS. 3 a .
  • a subject solution is placed within the upper reservoir chamber 28 of upper the compartment 14 , the cap 38 is secured in place as shown in FIG. 3 b , and the resulting unit is centrifuged (fixed angle or swinging bucket) or pressurized for as long as necessary (many times about 0.5 minute) to accomplish liquid movement through the unit.
  • the force moves the liquid quickly through the first membrane 24 as target molecules are collected.
  • this first membrane 24 has a relatively large pore size, virtually any sized molecules or micro-particulate can pass through unimpededly, and only target molecules or micro particulate with ionic, hydrophobic, or affinity attractions will be retained. Alternatively, dependent upon the properties of the passing solution, target molecules or micro-particulate may pass through the membrane while contaminant is retained.
  • the cap 38 is removed, an appropriate buffer solution is added to the upper compartment 14 which is re-capped, and a second period of centriftigation or pressurization is completed to assure removal of any contaminants from the target molecules, while the molecules or micro-particulate remain bound to the first membrane 24 . Elution of target molecules is accomplished as the independent compartment 36 with solute therein is removed and replaced with the lower compartment 16 as shown in FIG.
  • the upper reservoir chamber 28 is then filled with an appropriate elution buffer to remove the target molecules from the first membrane 24 and the separator device 10 is centrifuged for several minutes as the target molecules now pass through the first membrane 24 are captured because of size by the second membrane 26 .
  • the upper compartment 14 (FIG. 3 d ) is removed and, thereafter, the upper reservoir chamber 32 is filled with a final washing buffer and centrifuged for several minutes for product desalting and placing the target molecules in a desired buffer such as physiological saline.
  • an independent compartment 36 (FIG. 3 e ) is placed onto the compartment 16 , and the resulting unit is inverted and centrifuged or pressurized for final product collection as the target molecules are forced from the second membrane 26 and into the independent compartment 36 .
  • FIGS. 4 and 5 a - 5 g show a second preferred embodiment and use of a molecule or micro-particulate separator device 50 .
  • the separator device 50 includes a housing 52 constructed of two releasably connected, liquid-tight, separable compartments 54 , 56 , each having one separable reservoir 53 , 57 , with compartments 54 , 56 and reservoirs 53 , 57 held to each adjacent structure by conventional friction fit.
  • Within the housing 52 are two sequentially disposed membranes 63 , 65 for collecting two different filtrates.
  • the first membrane 63 is anisotropic (asymmetrical) and can be fabricated of any appropriate polymeric material with ultrafiltration pore size including nylon, polycarbonate, polyethersulfone, glass fiber, polypropylene, polysulfone, cellulose acetate, regenerated cellulose, and mixed esters of cellulose or polymeric materials as would be recognized by a skilled artisan while providing ultrafiltration in speaking toward molecular weight characteristics for capturing molecule filtrate.
  • a chosen molecular weight range can be exemplified in values from about 5 ⁇ 10 2 to about 3 ⁇ 10 6 Daltons.
  • the second membrane 65 is a chromatography membrane operating as a cationic or anionic ion-exchange membrane, hydrophobic membrane, affinity membrane, or a combination thereof for attracting molecules exhibiting ionic and/or hydrophobic and/or affinity attractions.
  • the second membrane 65 can have a porosity non-limitedly exemplified in the range of 0.1 to 10 microns and is also fabricated of nylon, polycarbonate, polyethersulfone, polysulfone, cellulose acetate, glass fiber, polypropylene, regenerated cellulose, and mixed esters of cellulose or other polymeric materials.
  • the upper compartment 54 of the housing 52 has an upper reservoir chamber 58 immediately above the first membrane 63 and a lower reservoir chamber 60 immediately below the first membrane 63 .
  • the lower compartment 56 includes an upper chamber 62 immediately above the second membrane 65 and a fluid collection chamber 64 immediately beneath the second membrane 65 .
  • the housing 52 can be constructed of a semi-rigid material such as polypropylene or of any other polymeric material as would be evident to a skilled artisan. Likewise, housing size can be as required to provide volumetric accommodations as required for a particular task. As is apparent, the housing 52 resembles the configuration of a standard centrifuge tube, thus permitting placement of the separator device 50 within a standard fixed-angle or swinging-bucket chamber (not shown) of a centrifuge head (not shown).
  • FIGS. 5 a - 5 g A description of an exemplary operation of the separator device 50 is accompanied by the illustrations of FIGS. 5 a - 5 g .
  • a subject solution is placed within the upper chamber 62 of the lower compartment 56 (FIG. 5 a ), the upper and lower compartments 54 , 56 are attached as shown in FIG. 5 b , and the resulting unit is centrifuged (fixed angle or swinging bucket) for as long as necessary (many times about 0.5 minute) to accomplish liquid movement through the membrane. As expected, the centrifugal force moves the liquid quickly through the second membrane 65 as target molecules are collected.
  • centrifuged fixed angle or swinging bucket
  • this second membrane 65 has a relatively large pore size, virtually any sized molecule or micro-particulate can pass through unimpededly, and only target molecules with ionic or hydrophobic or affinity attractions will be retained. Alternatively, dependent upon the properties of the passing solution, target molecules or micro-particulate may pass through the membrane while contaminant is retained.
  • an appropriate buffer solution is added to the upper chamber 62 of the lower compartment 56 , and a second centrifugation is completed to assure removal of any contaminants from the target molecules while the molecules remain bound to the second membrane 65 .
  • the reservoir 57 is then removed and emptied, and filled with an elution buffer. Upon reassembly, the separator device 50 is inverted (FIG.
  • the device 50 may be inverted at the beginning of the process such that the ultrafiltration membrane is the first contact membrane.
  • the molecule separator devices above described provide rapid two-stage separations within a single, convenient, and molecular-property specific apparatus. Additionally, as recognized by the skilled artisan, there are numerous possible combinations of chromatography membranes and ultrafiltration membranes for producing unique purification results. Therefore, while an illustrative and presently preferred embodiment of the invention has been described in detail herein, it is to be understood that the inventive concepts may be otherwise variously embodied and employed and that the appended claims are intended to be construed to include such variations except insofar as limited by prior art.

Abstract

A molecule separator device for isolating molecules having at least two separable properties and within a solution. The device includes a housing, and at least two molecule collection media disposed within the housing, whereby each such medium captures molecules exhibiting a respective property. In one embodiment, a first membrane captures only molecules with an ionic and/or hydrophobic and/or affinity attraction property while a second membrane captures only such molecules that additionally fall within a particular molecular weight range. A preferred housing is cylindrical for acceptance within a centrifuge, and is constructed of a plurality of releasably-connected compartments. The collection media is sequentially situated and centrifugation of the housing drives the solution through the media. Because of separation and subsequent collection in one device of molecules bearing multiple properties, the present invention permits rapid and efficient isolation of molecules and micro-particulate having a plurality of identification characteristics.

Description

CROSS REFERENCE TO RELATED APPLICATIONS
This application claims the benefits of U.S. Provisional Patent Application Ser. No. 60/193,118 filed Mar. 30, 2000, and of U.S. Provisional Patent Application Ser. No. 60/198,529 filed Apr. 20, 2000.
STATEMENT RE: FEDERALLY SPONSORED RESEARCH/DEVELOPMENT
Not Applicable
BACKGROUND OF THE INVENTION
This invention relates in general to the separation and capture of molecule types from a solution mixture thereof, and in particular to apparatus and methodology wherein molecules with two or more defined properties such as ionic, hydrophobic, or affinity attractions and molecular weight ranges are captured and retained first for one such property and thereafter for the additional property, with such respective collections accomplished sequentially in a single molecule separator device.
One of the most important tasks performed during research and other laboratory procedures is the separation of certain components from a mixture of components such that chemical or other analysis can proceed. A usual manner of accomplishing such separations is the employment of filtration devices whereby filtrate is collected by a filter medium as a solution containing the filtrate product passes through the filter medium. The most common of filter media are filter membranes and matrices thereof whose interstices prohibit, and thus capture, particulate whose physical size is too large to pass through as part of the solute.
While such filter membranes and related matrices (e.g. cloth) work well where particulate to be collected is defined only according to size and the interstices of the filter medium are adequately sized for filtrate retention, the separation of smaller particulate, as exemplified at the molecular level, requires much greater sophistication in order to accomplish separation and collection. Additionally, molecular separation many times involves the need to collect molecules that must possess at least two properties such as ionic, hydrophobic, or affinity attractions plus a limited molecular weight range. To accomplish separation and collection of such micro-particulate, multiple filtration devices must be employed where each device has a one-membrane-type filter for collecting filtrate having one defined characteristic from a solution. Once molecules are collected that possess the first desired property, the filtrate must be transferred to a second filtration device having a second one-membrane-type filter that addresses the second property and collects molecular filtrate meeting the second standard.
As is thus apparent, where, for example, molecules having at least two defining characteristics are to be isolated from a solution, a user must inefficiently perform filter procedures at least two separate times using at least two separate filtration devices. In view of this now-required inefficient approach, it is a primary object of the present invention to provide a molecule separator device where molecules having a plurality of properties can be separated and collected with one separator device.
Another object of the present invention to provide a molecule separator device where such molecule separation is accomplished sequentially within a single housing.
Yet another object of the present invention to provide a molecule separator device where respective dedicated membrane media provide filtrate collection.
Still another object of the present invention is to provide methodology for separating and capturing molecules having a plurality of properties utilizing a single separator device.
These and other objects of the present invention will become apparent throughout the description thereof which now follows.
BRIEF SUMMARY OF THE INVENTION
The present invention is a molecule separator device for separating and isolating molecules having at least two separable properties and present in a solution comprising the molecules. The separator device includes a housing for accepting pressured passage there through of the solution, and at least two molecule collection media disposed within the housing, wherein each such medium captures molecules exhibiting a respective property respectively capturable by the media. In a preferred embodiment, a first molecule-collection chromatography membrane captures and retains only molecules with an ionic, hydrophobic, or affinity attraction property while a second molecule-collection ultrafiltration membrane captures and retains additional such molecules that additionally fall within a particular molecular weight range. Conversely, these exemplary membranes can be in reverse order such that the first molecular collection membrane is an ultrafiltration membrane while the second membrane possesses the ionic, hydrophobic, or affinity attraction property. A preferred housing is generally cylindrical for operational acceptance within a generally cylindrical fixed-angle or swinging-bucket chamber of a centrifuge head, and is constructed of a plurality of liquid-tight, releasably-connected compartments in communication with each other. The collection media is situated in a sequential relationship among the compartments while centrifugation of the housing drives the solution through the media. Removing and replacing appropriate compartments during the molecule collection process permits separate and replaceable reservoir, wash, and collection sites to yield filtrate product as so chosen for further analysis, processing, or use, or for discard where a separation goal is the provision of clean solute. Because of separation and subsequent collection of molecules bearing two or more properties, the present invention permits rapid and efficient isolation of molecules and/or micro-particulate having multiple identification characteristics.
BRIEF SUMMARY OF THE DRAWINGS
An illustrative and presently preferred embodiment of the invention is shown in the accompanying drawings in which:
FIG. 1 is a perspective view of a first embodiment of a molecule separator device for capture or collection of molecules and/or micro-particulate;
FIG. 2 is a perspective view of a separated compartment structure for the separator device of FIG. 1;
FIGS. 3a-3 e illustrate use of the embodiment of FIG. 1;
FIG. 4 is a side perspective view of a second embodiment of a molecule separator device; and
FIGS. 5a-5 g illustrate use of the embodiment of FIG. 4.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring first to FIGS. 1 and 2, a molecule separator device 10 is shown. The device 10 includes a housing 12 constructed of two releasably connected, liquid-tight, separable compartments 14, 16 attached to each other by conventional friction fit between adjacent compartments. Within the housing 12 are two sequentially disposed membranes 24, 26 for collecting filtrates. In particular, the first membrane 24 is a chromatography membrane operating as a cationic or anionic ion-exchange membrane, hydrophobic membrane, affinity membrane, or a combination thereof for attracting molecules exhibiting ionic and/or hydrophobic and/or affinity attractions. The first membrane 24 can have a porosity non-limitedly exemplified in the range of 0.1 to 10 microns and is fabricated of any appropriate microporous material including nylon, polycarbonate, polyethersulfone, glass fiber, polypropylene, polysulfone, cellulose acetate, regenerated cellulose, and mixed esters of cellulose or other polymeric material as would be recognized by a skilled artisan. The second membrane 26 preferably is anisotropic (asymmetrical) and can be fabricated of the same materials as the first while providing ultrafiltration in speaking toward molecular weight characteristics for capturing molecule filtrate. Thus, a chosen molecular weight range can be exemplified in values from about 5×102 to about 3×106 Daltons.
As shown in FIG. 1, the upper compartment 14 of the housing 12 has an upper reservoir chamber 28 immediately above the first membrane 24 and a lower reservoir chamber 30 immediately below the first membrane 24. The lower compartment 16 includes an upper chamber 32 immediately above the second membrane 26 and a fluid collection chamber 34 immediately beneath the second membrane 26. FIG. 2 shows an independent compartment 36 attachable to the upper compartment 14 during certain washing procedures as described later. The housing 12 can be constructed of a semi-rigid material such as polypropylene or of any other plastic or polymeric material as would be evident to a skilled artisan. Likewise, housing size can be as required to provide volumetric accommodations as required for a particular task. A screw-type closure cap 38 with an aperture 40 there through closes the housing 12. As is apparent, the housing 12 resembles the configuration of a standard centrifuge tube, thus permitting placement of the separator device 10 within a standard fixed-angle or swinging-bucket chamber (not shown) of a centrifuge head (not shown). While centrifugation is the preferred manner of pressurized force, the aperture 40 in the screw cap 38 is provided to accept a pressure nozzle such as the outlet of a hypodermic syringe (not shown) whose pressure can be applied to force the solution through the separator device 10.
A description of an exemplary operation of the separator device 10 is accompanied by the illustrations of FIGS. 3a-3 e. First, the upper compartment 14 and an independent compartment 36 are attached as shown in FIGS. 3a. A subject solution is placed within the upper reservoir chamber 28 of upper the compartment 14, the cap 38 is secured in place as shown in FIG. 3b , and the resulting unit is centrifuged (fixed angle or swinging bucket) or pressurized for as long as necessary (many times about 0.5 minute) to accomplish liquid movement through the unit. As expected, the force moves the liquid quickly through the first membrane 24 as target molecules are collected. Since this first membrane 24 has a relatively large pore size, virtually any sized molecules or micro-particulate can pass through unimpededly, and only target molecules or micro particulate with ionic, hydrophobic, or affinity attractions will be retained. Alternatively, dependent upon the properties of the passing solution, target molecules or micro-particulate may pass through the membrane while contaminant is retained. The cap 38 is removed, an appropriate buffer solution is added to the upper compartment 14 which is re-capped, and a second period of centriftigation or pressurization is completed to assure removal of any contaminants from the target molecules, while the molecules or micro-particulate remain bound to the first membrane 24. Elution of target molecules is accomplished as the independent compartment 36 with solute therein is removed and replaced with the lower compartment 16 as shown in FIG. 3c. The upper reservoir chamber 28 is then filled with an appropriate elution buffer to remove the target molecules from the first membrane 24 and the separator device 10 is centrifuged for several minutes as the target molecules now pass through the first membrane 24 are captured because of size by the second membrane 26. The upper compartment 14 (FIG. 3d) is removed and, thereafter, the upper reservoir chamber 32 is filled with a final washing buffer and centrifuged for several minutes for product desalting and placing the target molecules in a desired buffer such as physiological saline. Finally, an independent compartment 36 (FIG. 3e) is placed onto the compartment 16, and the resulting unit is inverted and centrifuged or pressurized for final product collection as the target molecules are forced from the second membrane 26 and into the independent compartment 36.
FIGS. 4 and 5a-5 g show a second preferred embodiment and use of a molecule or micro-particulate separator device 50. In particular, the separator device 50 includes a housing 52 constructed of two releasably connected, liquid-tight, separable compartments 54, 56, each having one separable reservoir 53, 57, with compartments 54, 56 and reservoirs 53, 57 held to each adjacent structure by conventional friction fit. Within the housing 52 are two sequentially disposed membranes 63, 65 for collecting two different filtrates. In particular, the first membrane 63 is anisotropic (asymmetrical) and can be fabricated of any appropriate polymeric material with ultrafiltration pore size including nylon, polycarbonate, polyethersulfone, glass fiber, polypropylene, polysulfone, cellulose acetate, regenerated cellulose, and mixed esters of cellulose or polymeric materials as would be recognized by a skilled artisan while providing ultrafiltration in speaking toward molecular weight characteristics for capturing molecule filtrate. Thus, a chosen molecular weight range can be exemplified in values from about 5×102 to about 3×106 Daltons. The second membrane 65 is a chromatography membrane operating as a cationic or anionic ion-exchange membrane, hydrophobic membrane, affinity membrane, or a combination thereof for attracting molecules exhibiting ionic and/or hydrophobic and/or affinity attractions. The second membrane 65 can have a porosity non-limitedly exemplified in the range of 0.1 to 10 microns and is also fabricated of nylon, polycarbonate, polyethersulfone, polysulfone, cellulose acetate, glass fiber, polypropylene, regenerated cellulose, and mixed esters of cellulose or other polymeric materials.
As shown in FIG. 4, the upper compartment 54 of the housing 52 has an upper reservoir chamber 58 immediately above the first membrane 63 and a lower reservoir chamber 60 immediately below the first membrane 63. The lower compartment 56 includes an upper chamber 62 immediately above the second membrane 65 and a fluid collection chamber 64 immediately beneath the second membrane 65. The housing 52 can be constructed of a semi-rigid material such as polypropylene or of any other polymeric material as would be evident to a skilled artisan. Likewise, housing size can be as required to provide volumetric accommodations as required for a particular task. As is apparent, the housing 52 resembles the configuration of a standard centrifuge tube, thus permitting placement of the separator device 50 within a standard fixed-angle or swinging-bucket chamber (not shown) of a centrifuge head (not shown).
A description of an exemplary operation of the separator device 50 is accompanied by the illustrations of FIGS. 5a-5 g. First, a subject solution is placed within the upper chamber 62 of the lower compartment 56 (FIG. 5a), the upper and lower compartments 54, 56 are attached as shown in FIG. 5b, and the resulting unit is centrifuged (fixed angle or swinging bucket) for as long as necessary (many times about 0.5 minute) to accomplish liquid movement through the membrane. As expected, the centrifugal force moves the liquid quickly through the second membrane 65 as target molecules are collected. Since this second membrane 65 has a relatively large pore size, virtually any sized molecule or micro-particulate can pass through unimpededly, and only target molecules with ionic or hydrophobic or affinity attractions will be retained. Alternatively, dependent upon the properties of the passing solution, target molecules or micro-particulate may pass through the membrane while contaminant is retained. Next, an appropriate buffer solution is added to the upper chamber 62 of the lower compartment 56, and a second centrifugation is completed to assure removal of any contaminants from the target molecules while the molecules remain bound to the second membrane 65. The reservoir 57 is then removed and emptied, and filled with an elution buffer. Upon reassembly, the separator device 50 is inverted (FIG. 5e) and inserted into the centrifuge for centrifugation to remove the target molecules or micro-particulate from the second membrane 65 and capture them because of size at the first membrane 63. Thereafter, while remaining in the now-upside down position, the lower reservoir chamber 60 is filled with an appropriate buffer to wash the target molecules free of high salt of the elution buffer while retaining the molecules at the first membrane 54. Finally, the reservoir 53 is emptied (FIG. 5f), the reservoir 57 is removed and replaced with a new reservoir 57 a (FIG. 5g), and the resulting unit is inverted and centrifuged for final product collection as the target molecules are forced into the reservoir 57 a. Alternatively, of course, the device 50 may be inverted at the beginning of the process such that the ultrafiltration membrane is the first contact membrane.
As is apparent, the molecule separator devices above described provide rapid two-stage separations within a single, convenient, and molecular-property specific apparatus. Additionally, as recognized by the skilled artisan, there are numerous possible combinations of chromatography membranes and ultrafiltration membranes for producing unique purification results. Therefore, while an illustrative and presently preferred embodiment of the invention has been described in detail herein, it is to be understood that the inventive concepts may be otherwise variously embodied and employed and that the appended claims are intended to be construed to include such variations except insofar as limited by prior art.

Claims (18)

What is claimed is:
1. A molecule separator device for separation and isolating target molecules in a solution, the separator device comprising:
a reversible first compartment, further comprising:
a first molecule-collection medium operative to collect the target molecules with a first separation property; and
two chambers immediately adjacent to two sides of the first molecule-collection medium; and
a reversible second compartment connectible to and separable from the first compartment, the second compartment further comprising:
a second molecule collection medium operative to collect the target molecules with a second separation property different from the first separation property; and
two chambers immediately adjacent to two sides of the second molecule collection medium.
2. A molecule separator device as claimed in claim 1 wherein both the first and second molecule-collection media are membranes.
3. A molecule separator device as claimed in claim 1 wherein the first molecule collection-medium captures the target molecules exhibiting the first separation property of ion and/or hydrophobic and/or affinity attraction.
4. A molecule separator device as claimed in claim 3 wherein the second molecule-collection medium captures the target molecules exhibiting the second separation property of molecular weight property from about 5×102 to about 3×106 Daltons.
5. A molecule separator device as claimed in claim 1 wherein the second molecule-collection medium captures the target molecules exhibiting the second separation property of molecular weight property from about 5×102 to about 3×106 Daltons.
6. A molecule separator device as claimed in claim 5 wherein the second molecule-collection medium is fabricated of material selected from the group consisting of nylon, polycarbonate, polyethersulfone, polysulfone, glass fiber, polypropylene, cellulose acetate, regenerated cellulose, and mixed esters of cellulose.
7. A molecule separator device as claimed in claim 6 wherein the second molecule-collection medium is anisotropic.
8. A molecule separator device as claimed in claim 1 wherein the first and second molecule-collection media are disposed sequentially in relation to each other.
9. A molecule separator device as claimed in claim 1 wherein at least one of the first and second molecule-collection media are reversely disposed to collect the target molecules captured thereby.
10. A molecule separator device as claimed in claim 7 wherein at least one of the first and second molecule-collection media are reversely disposed to receive an elution solution for recollecting the captured molecules.
11. A molecule separator device as claimed in claim 3 wherein the first molecule-collection medium is at least an ion-exchange membrane, a hydrophobic membrane, an affinity membrane or a combination of any two or all three thereof.
12. A molecule separator device as claimed in claim 11 wherein the first molecule-collection medium is fabricated of material selected from the group consisting of nylon, polycarbonate, polyethersulfone, polysulfone, glass fiber, polypropylene, cellulose acetate, regenerated cellulose, and mixed esters of cellulose.
13. A molecule separator device as claimed in claim 12 wherein the second molecule-collection medium is fabricated of material selected from the group consisting of nylon, polycarbonate, polyethersulfone, polysulfone, glass fiber, polypropylene, cellulose acetate, regenerated cellulose, and mixed esters of cellulose.
14. A molecule separator device as claimed in claim 1 wherein the first and second reversible compartments are connected to form a generally cylindrical liquid-tight housing for operational acceptance within a generally cylindrical fixed-angle or swinging-bucket chamber of a centrifuge head.
15. A molecule separator device as claimed in claim 14 wherein the first and second compartments are in communication with each other while being connected to form the housing.
16. A molecule separator device as claimed in claim 15 wherein the housing additionally comprises a releasably-connected cap with an aperture there through for receiving a fluid or gas pressurization nozzle.
17. A molecule separator device for separation and isolating target molecules in a solution, the separator device comprising:
a first compartment, further comprising:
a first molecule collecting medium operative to collect the molecules with a first separation property; and
two chambers immediately adjacent to two sides of the first molecule collecting medium;
a second compartment liquid-tight connectible to and separable from the first compartment, the second compartment further comprising:
a second molecule collecting medium operative to collect the molecules with a second separation property different from the first separation property; and
two chambers immediately adjacent to two sides of the second molecule collecting medium; and
an reversible independent chamber, liquid-tight connectible to the first and second compartments.
18. A molecule separator device as claimed in claim 17 wherein the first molecule-collection medium includes a chromatography membrane, and the second molecule-collection medium includes a weight ultrafiltration membrane.
US09/818,468 2000-03-30 2001-03-27 Molecule separation device and method combining multiple filtration media Expired - Fee Related US6602414B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US09/818,468 US6602414B2 (en) 2000-03-30 2001-03-27 Molecule separation device and method combining multiple filtration media
US10/460,280 US7045064B2 (en) 2000-03-30 2003-06-12 Molecule separation device and method combining multiple filtration media

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US19311800P 2000-03-30 2000-03-30
US19852900P 2000-04-20 2000-04-20
US09/818,468 US6602414B2 (en) 2000-03-30 2001-03-27 Molecule separation device and method combining multiple filtration media

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US10/460,280 Division US7045064B2 (en) 2000-03-30 2003-06-12 Molecule separation device and method combining multiple filtration media

Publications (2)

Publication Number Publication Date
US20010025818A1 US20010025818A1 (en) 2001-10-04
US6602414B2 true US6602414B2 (en) 2003-08-05

Family

ID=26888685

Family Applications (2)

Application Number Title Priority Date Filing Date
US09/818,468 Expired - Fee Related US6602414B2 (en) 2000-03-30 2001-03-27 Molecule separation device and method combining multiple filtration media
US10/460,280 Expired - Fee Related US7045064B2 (en) 2000-03-30 2003-06-12 Molecule separation device and method combining multiple filtration media

Family Applications After (1)

Application Number Title Priority Date Filing Date
US10/460,280 Expired - Fee Related US7045064B2 (en) 2000-03-30 2003-06-12 Molecule separation device and method combining multiple filtration media

Country Status (2)

Country Link
US (2) US6602414B2 (en)
GB (1) GB2360715B (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020106310A1 (en) * 1998-12-23 2002-08-08 Peter Zuk Apparatus comprising a disposable device and reusable instrument for synthesizing chemical compounds, and for testing chemical compounds for solubility
US20040004039A1 (en) * 2000-03-30 2004-01-08 Warner Timothy Neal Molecule separation device and method combining multiple filtration media
US20040053422A1 (en) * 2002-09-17 2004-03-18 Selena Chan Microfluidic devices with porous membranes for molecular sieving, metering, and separations
US20040136874A1 (en) * 2001-05-05 2004-07-15 Ingo Klimant Method and device for identifying volatile substances in solution
US20050026175A1 (en) * 2003-07-31 2005-02-03 John Link Devices and methods for isolating RNA
US20050038562A1 (en) * 2003-08-13 2005-02-17 Bash Cullen E. Semi-autonomous operation of a robotic device
US20050042660A1 (en) * 2003-07-31 2005-02-24 Hall Gerald Edward Devices and methods for isolating RNA
US20060099605A1 (en) * 2004-11-11 2006-05-11 Hall Gerald E Jr Devices and methods for isolating RNA
US20060223072A1 (en) * 2005-03-31 2006-10-05 Boyes Barry E Methods of using a DNase I-like enzyme
US20060223073A1 (en) * 2005-03-31 2006-10-05 Boyes Barry E Methods of using a DNase I-like enzyme
US20060270843A1 (en) * 2005-05-26 2006-11-30 Hall Gerald E Jr Methods for isolation of nucleic acids
WO2015065924A3 (en) * 2013-10-28 2015-10-29 Massachusetts Institute Of Technology Hydrogel microstructures with immiscible fluid isolation for small reaction volumes
US9199250B2 (en) 2009-05-01 2015-12-01 Trustees Of Boston University Disposable separator/concentrator device and method of use

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040236083A1 (en) * 2003-05-14 2004-11-25 Libert Sharon Ann Protein separation column
EP1752651A1 (en) * 2005-08-09 2007-02-14 Delphi Technologies, Inc. Fuel injection system
EP1752652A1 (en) * 2005-08-09 2007-02-14 Delphi Technologies, Inc. Fuel injection system
US20070102358A1 (en) * 2005-11-09 2007-05-10 Cera Inc. Solid phase extraction column
US8357296B2 (en) 2007-09-24 2013-01-22 Emd Millipore Corporation Centrifugal filter
US9304070B2 (en) 2011-07-13 2016-04-05 Emd Millipore Corporation All-in-one sample preparation device and method
CN108601565B (en) * 2015-12-11 2021-09-07 巴布森诊断公司 Sample container and method for separating serum or plasma from whole blood
US11241657B2 (en) 2019-11-22 2022-02-08 Pall Corporation Filter for removing silica from ultra pure water and method of use
WO2022076692A1 (en) * 2020-10-08 2022-04-14 Lmx Medtech Llc Method for sample collection and metering
US20230331773A1 (en) * 2022-04-15 2023-10-19 Pall Corporation Chromatography device and method of use

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4755301A (en) 1983-08-15 1988-07-05 W. R. Grace & Co. Apparatus and method for centrifugal recovery of retentate
US4769145A (en) * 1984-03-21 1988-09-06 Toyo Soda Manufacturing Co., Ltd. Centrifugal ultrafilter unit for ultrafiltration of biochemical solutions
US4935142A (en) * 1989-06-23 1990-06-19 Memtek Corporation Apparatus for retaining variable number of sheet membrane elements and a method for the use thereof
US5215657A (en) * 1991-07-03 1993-06-01 Goldfield H P Water treatment system
US5368729A (en) * 1993-07-23 1994-11-29 Whatman, Inc. Solid phase extraction device
US5490927A (en) * 1995-01-04 1996-02-13 Filtron Technology Corporation Filtration apparatus with membrane filter unit
US5733449A (en) * 1995-12-08 1998-03-31 Orbital Biosciences, Llc Microconcentrator device
US5792425A (en) * 1995-05-19 1998-08-11 Millipore Coporation Vacuum filter device
US5833860A (en) 1995-08-28 1998-11-10 Millipore Investment Holdings Limited Centrifugal adsorptive sample preparation device and method
US5861094A (en) * 1997-04-17 1999-01-19 Goehde; Wolfgang Filter for biological particle separation
US6103195A (en) * 1997-08-08 2000-08-15 Shukla; Ashok K. Micro-volume spin columns for sample preparation
US6171869B1 (en) 1997-04-08 2001-01-09 Beckman Coulter, Inc. Process for desalting and concentrating protein-containing solutions
US6221655B1 (en) * 1998-08-01 2001-04-24 Cytosignal Spin filter assembly for isolation and analysis

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2008354A1 (en) * 1970-02-23 1971-09-09 Boehnnger Mannheim GmbH, 6800 Mann heim Combination column
US4636361A (en) * 1985-11-18 1987-01-13 Miklos Marian Device for separating liquid fractions
US5112490A (en) * 1986-02-19 1992-05-12 Jon Turpen Sample filtration, separation and dispensing device
US5124041A (en) * 1989-07-28 1992-06-23 Applied Biosystems, Inc. Biomolecule sample immobilization
CA2059398C (en) * 1991-02-07 1999-05-25 Craig G. Markell Solid phase extraction medium
US5834229A (en) * 1991-05-24 1998-11-10 Genentech, Inc. Nucleic acids vectors and host cells encoding and expressing heregulin 2-α
DE4309410A1 (en) * 1993-03-19 1995-02-16 Stange Jan Material, process and equipment for the selective separation of freely dissolved and substance-bound substances from liquid substance mixtures as well as process for the production of the material
AU2278895A (en) * 1994-04-08 1995-10-30 Amicon, Inc. Apparatus for isolation and purification of biologically active compounds
EP0709132A1 (en) * 1994-10-28 1996-05-01 MEMBRANE SEPARATION TECHNOLOGIES S.r.L. Fluid filtration device
US6359114B1 (en) * 1995-06-07 2002-03-19 Aphton Corp. System for method for the modification and purification of proteins
CN1378592A (en) * 1999-07-23 2002-11-06 杰南技术公司 Method for RNA ase-and organic solvent-free plasmid DNA purification using tangential flow filtration
US6602414B2 (en) * 2000-03-30 2003-08-05 Formulations Pro Molecule separation device and method combining multiple filtration media

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4755301A (en) 1983-08-15 1988-07-05 W. R. Grace & Co. Apparatus and method for centrifugal recovery of retentate
US4769145A (en) * 1984-03-21 1988-09-06 Toyo Soda Manufacturing Co., Ltd. Centrifugal ultrafilter unit for ultrafiltration of biochemical solutions
US4935142A (en) * 1989-06-23 1990-06-19 Memtek Corporation Apparatus for retaining variable number of sheet membrane elements and a method for the use thereof
US5215657A (en) * 1991-07-03 1993-06-01 Goldfield H P Water treatment system
US5368729A (en) * 1993-07-23 1994-11-29 Whatman, Inc. Solid phase extraction device
US5490927A (en) * 1995-01-04 1996-02-13 Filtron Technology Corporation Filtration apparatus with membrane filter unit
US5792425A (en) * 1995-05-19 1998-08-11 Millipore Coporation Vacuum filter device
US5833860A (en) 1995-08-28 1998-11-10 Millipore Investment Holdings Limited Centrifugal adsorptive sample preparation device and method
US5733449A (en) * 1995-12-08 1998-03-31 Orbital Biosciences, Llc Microconcentrator device
US6171869B1 (en) 1997-04-08 2001-01-09 Beckman Coulter, Inc. Process for desalting and concentrating protein-containing solutions
US5861094A (en) * 1997-04-17 1999-01-19 Goehde; Wolfgang Filter for biological particle separation
US6103195A (en) * 1997-08-08 2000-08-15 Shukla; Ashok K. Micro-volume spin columns for sample preparation
US6221655B1 (en) * 1998-08-01 2001-04-24 Cytosignal Spin filter assembly for isolation and analysis

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6951762B2 (en) * 1998-12-23 2005-10-04 Zuk Jr Peter Apparatus comprising a disposable device and reusable instrument for synthesizing chemical compounds, and for testing chemical compounds for solubility
US20020106310A1 (en) * 1998-12-23 2002-08-08 Peter Zuk Apparatus comprising a disposable device and reusable instrument for synthesizing chemical compounds, and for testing chemical compounds for solubility
US7045064B2 (en) * 2000-03-30 2006-05-16 Timothy Neal Warner Molecule separation device and method combining multiple filtration media
US20040004039A1 (en) * 2000-03-30 2004-01-08 Warner Timothy Neal Molecule separation device and method combining multiple filtration media
US20040136874A1 (en) * 2001-05-05 2004-07-15 Ingo Klimant Method and device for identifying volatile substances in solution
US7390673B2 (en) * 2001-05-05 2008-06-24 Merck Patent Gmbh Method and device for identifying volatile substances in solution
US20040053422A1 (en) * 2002-09-17 2004-03-18 Selena Chan Microfluidic devices with porous membranes for molecular sieving, metering, and separations
US7279134B2 (en) * 2002-09-17 2007-10-09 Intel Corporation Microfluidic devices with porous membranes for molecular sieving, metering, and separations
US20050026175A1 (en) * 2003-07-31 2005-02-03 John Link Devices and methods for isolating RNA
US20050042660A1 (en) * 2003-07-31 2005-02-24 Hall Gerald Edward Devices and methods for isolating RNA
US7031802B2 (en) 2003-08-13 2006-04-18 Hewlett-Packard Development Company, L.P. Semi-autonomous operation of a robotic device
US20050038562A1 (en) * 2003-08-13 2005-02-17 Bash Cullen E. Semi-autonomous operation of a robotic device
US20060099605A1 (en) * 2004-11-11 2006-05-11 Hall Gerald E Jr Devices and methods for isolating RNA
US20060223072A1 (en) * 2005-03-31 2006-10-05 Boyes Barry E Methods of using a DNase I-like enzyme
US20060223073A1 (en) * 2005-03-31 2006-10-05 Boyes Barry E Methods of using a DNase I-like enzyme
US20060270843A1 (en) * 2005-05-26 2006-11-30 Hall Gerald E Jr Methods for isolation of nucleic acids
US9199250B2 (en) 2009-05-01 2015-12-01 Trustees Of Boston University Disposable separator/concentrator device and method of use
WO2015065924A3 (en) * 2013-10-28 2015-10-29 Massachusetts Institute Of Technology Hydrogel microstructures with immiscible fluid isolation for small reaction volumes
US9937495B2 (en) 2013-10-28 2018-04-10 Massachusetts Institute Of Technology Hydrogel microstructures with immiscible fluid isolation for small reaction volumes

Also Published As

Publication number Publication date
US20010025818A1 (en) 2001-10-04
GB0108008D0 (en) 2001-05-23
US7045064B2 (en) 2006-05-16
GB2360715B (en) 2004-02-18
US20040004039A1 (en) 2004-01-08
GB2360715A (en) 2001-10-03

Similar Documents

Publication Publication Date Title
US6602414B2 (en) Molecule separation device and method combining multiple filtration media
US3488768A (en) Self-cleaning ultrafilter
EP0651675B1 (en) Centrifugal method for concentrating macromolecules from a solution and device for carrying out said method
US7240572B2 (en) Vacuum assisted affinity chromatography device and method
US3481477A (en) Apparatus for filtering out clear liquid from suspended solids
US8980107B2 (en) Spin filter
US6375855B1 (en) Method, device and apparatus for concentrating and/or purifying macromolecules in a solution
US6659975B2 (en) Plasma collecting device
US20050145581A1 (en) Underdrain for filtration membrane
JPH07500914A (en) Cell centrifugation instruments, devices and methods
EP2260300B1 (en) Method and device for particle removal and droplet preparation for qualitative and quantitative bioanalysis
WO1999022850A1 (en) Membrane purification device
US20140246389A1 (en) Filter Arrangement and Method for Using the Same
US4647376A (en) Device for removing the liquid phase from a suspension
US20010035375A1 (en) Filter for arrayable micro-centrifuge
US6375856B1 (en) Method of recovering blood filtration residues
CN110857904A (en) Method for obtaining plasma from whole blood sample, hemofilter and microfluidic chip
JP5785713B2 (en) Leukocyte fraction collection device
JP4078460B2 (en) Plasma separation filter, plasma separation method and plasma separation apparatus using the same
JP2538751B2 (en) Leukocyte capture and separation device
US20020185429A1 (en) Filter for arrayable micro-centrifuge
JP3551080B2 (en) Separation device
JPH01224324A (en) Leukocyte-separating material
JPH0645546B2 (en) White blood cell separation material manufacturing method
US20240053237A1 (en) Device and method for separating particles of different sizes in a liquid, and applications of the device

Legal Events

Date Code Title Description
AS Assignment

Owner name: FORMULATION PRO, CALIFORNIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:WARNER, TIMOTHY NEAL;REEL/FRAME:011647/0200

Effective date: 20010326

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362

FP Lapsed due to failure to pay maintenance fee

Effective date: 20070805